WO2008073662A1 - Electrospinning process - Google Patents

Electrospinning process Download PDF

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Publication number
WO2008073662A1
WO2008073662A1 PCT/US2007/084381 US2007084381W WO2008073662A1 WO 2008073662 A1 WO2008073662 A1 WO 2008073662A1 US 2007084381 W US2007084381 W US 2007084381W WO 2008073662 A1 WO2008073662 A1 WO 2008073662A1
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WIPO (PCT)
Prior art keywords
polymer
groups
meth
weight
percent
Prior art date
Application number
PCT/US2007/084381
Other languages
French (fr)
Inventor
Stuart D. Hellring
Kaliappa G. Ragunathan
Kenneth J. Balog
Original Assignee
Ppg Industries Ohio, Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ppg Industries Ohio, Inc. filed Critical Ppg Industries Ohio, Inc.
Priority to CN200780046137.9A priority Critical patent/CN101558189B/en
Priority to AU2007333369A priority patent/AU2007333369B2/en
Priority to EP07864252A priority patent/EP2102394B1/en
Priority to JP2009541448A priority patent/JP2010512472A/en
Priority to DE602007009320T priority patent/DE602007009320D1/en
Priority to MX2009006204A priority patent/MX2009006204A/en
Priority to AT07864252T priority patent/ATE481513T1/en
Priority to BRPI0719721-7A priority patent/BRPI0719721A2/en
Priority to CA002671499A priority patent/CA2671499A1/en
Publication of WO2008073662A1 publication Critical patent/WO2008073662A1/en

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Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/0007Electro-spinning
    • D01D5/0015Electro-spinning characterised by the initial state of the material
    • D01D5/0053Electro-spinning characterised by the initial state of the material the material being a low molecular weight compound or an oligomer, and the fibres being formed by self-assembly
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/0007Electro-spinning
    • D01D5/0015Electro-spinning characterised by the initial state of the material
    • D01D5/003Electro-spinning characterised by the initial state of the material the material being a polymer solution or dispersion
    • D01D5/0038Electro-spinning characterised by the initial state of the material the material being a polymer solution or dispersion the fibre formed by solvent evaporation, i.e. dry electro-spinning
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/38Formation of filaments, threads, or the like during polymerisation
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/28Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F6/36Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds comprising unsaturated carboxylic acids or unsaturated organic esters as the major constituent
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/29Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
    • Y10T428/2913Rod, strand, filament or fiber
    • Y10T428/298Physical dimension

Definitions

  • the present invention relates to an electrospinning process, the resulting electrospun fiber and polymers used in the electrospinning process.
  • the process of electrospinning uses an electrical charge to form fine fibers.
  • the process consists of a spinneret with a dispensing needle, a syringe pump, a power supply and a grounded collection device.
  • Polymers in solution or as melts are located in the syringe and driven to the needle tip by the syringe pump where they form a droplet.
  • a droplet is stretched to an electrified liquid jet.
  • the jet is elongated continuously until it is deposited on the collector as a mat of fine fibers usually of nanometer-sized dimensions.
  • the resultant fibers are useful in a wide variety of applications such as protective clothing, wound dressing and as supports or carriers for catalyst.
  • the polymeric melt or solution must have a sufficient viscosity otherwise a drop rather than a liquid jet will form.
  • thickeners are included in the polymer solution or melt to provide the necessary viscosity.
  • thickeners can adversely affect the properties of the resultant fibers and for this reason, their use should be minimized.
  • the present invention provides for a process of electrospinning a fiber from an electrically conductive solution of a polymer in the presence of an electric field between a spinneret and a ground source.
  • the polymer undergoes a crosslinking reaction prior to and during the electrospinning process resulting in a viscosity buildup of the polymer solution enabling fiber formation and minimizing the use of thickeners.
  • the invention also provides for the resultant eiectrospun fiber that contains silane, preferably carboxyl and hydroxyl groups and optionally a nitrogen-containing group such as amine or amide groups.
  • silane groups provide for crosslinking and viscosity build-up.
  • carboxyl, hydroxyl, amine and amide groups provide for a hydrogen bonding and viscosity build-up.
  • the carboxyl group, in the form of carboxylic acid, and the nitrogen-containing groups are good electrical charge carrying groups.
  • FIG. 1 depicts a basic electrospinning system
  • FIG. 2 simulates a scanning electron microscopic (SCM) image of a non-woven mat.
  • each numerical parameter shouid at least be construed in light of the number of reported significant digits and by applying ordinary rounding techniques. Notwithstanding that the numerical ranges and parameters setting forth the broad scope of the invention are approximations, the numerical values set forth in the specific examples are reported as precisely as possible. Any numerical value, however, inherently contains certain errors necessarily resulting from the standard variation found in their respective testing measurements. [0008] Also, it should be understood that any numerical range recited herein is intended to include all sub-ranges subsumed therein.
  • a range of "1 to 10" is intended to include all sub-ranges between (and including) the recited minimum value of 1 and the recited maximum value of 10, that is, having a minimum value equal to or greater than 1 and a maximum value of equal to or less than 10.
  • the electrospinning system consists of three major components, a power supply 1 , a spinneret 3 and an electrically grounded collector 4. Direct current or alternating current may be used in the electrospinning process.
  • the polymer solution 5 is contained in a syringe 7.
  • a syringe pump 9 forces the solution through the spinneret 3 at a controlled rate.
  • a drop of the solution forms at the tip of the needle 1 1.
  • a voltage typically from 5 to 30 kilovolts (kV)
  • kV kilovolts
  • the polymers of the present invention can be acrylic polymers.
  • acrylic polymer refers to those polymers that are well known to those skilled in the art which results in the polymerization of one or more ethylenically unsaturated polymerizable materials.
  • (Meth)acrylic polymers suitable for use in the present invention can be made by any of a wide variety of methods as will be understood by those skilled in the art.
  • the (meth)acrylic polymers can be made by addition polymerization of unsaturated polymerizable materials that contain silane groups, carboxyl groups, hydroxyl groups and optionally a nitrogen-containing group.
  • silane groups include, without limitation, groups that have the structure Si-X n (wherein n is an integer having a value ranging from 1 to 3 and X is selected from chlorine, alkoxy esters, and/or acyloxy esters). Such groups hydroiyze in the presence of water including moisture in the air to form silanol groups that condense to form -Si-O-Si- groups.
  • silane-containing ethylenically unsaturated polymerizable materials suitable for use in preparing such (meth)acrylic polymers include, without limitation, ethylenically unsaturated alkoxy siianes and ethylenically unsaturated acyloxy siianes, more specific examples of which include vinyf siianes such as vinyl trimethoxysilane, acrylatoalkoxysilanes, such as gamma-acryloxypropyl trimethoxysilane and gamma-acryloxypropyl triethoxysilane, and methacrylatoalkoxysilanes, such as gamma-methacryloxypropyl trimethoxysilane, gamma-methacryloxypropyl triethoxysilane and gamma-methacryloxypropy!
  • vinyf siianes such as vinyl trimethoxysilane
  • acrylatoalkoxysilanes such as gam
  • acyloxysilanes including, for example, acryfato acetoxys ⁇ anes, methacrylato acetoxysilanes and ethylenically unsaturated acetoxysilanes, such as acrylatopropyl triacetoxysilane and methacrylatopropyi triacetoxysilane.
  • monomers that, upon addition polymerization, will result in a (meth)acrylic polymer in which the Si atoms of the resulting hydrolyzable silyl groups are separated by at least two atoms from the backbone of the polymer.
  • Preferred monomers are (meth)acryloxyaikylpolyalkoxy silane, particularly (meth)acryloxyalkyltrialkoxy silane in which the alkyl group contains from 2 to 3 carbon atoms and the alkoxy groups contain from 1 to 2 carbon atoms.
  • the amount of the silane-containing ethylenically unsaturated polymerizable material used in the total monomer mixture is chosen so as to result in the production of a (meth)acrylic polymer comprising silane groups that contain from 0.2 to 20, preferably 5 to 10 percent by weight, silicon, based on the weight of the total monomer combination used in preparing the (meth)acryiic polymer.
  • the (meth)acrylic polymer suitable for use in the present invention can be the reaction product of one or more of the aforementioned silane-containing ethylenically unsaturated polymerizable materials and preferably an ethylenically unsaturated poiymerizable material that comprises carboxyl such as carboxylic acid groups or an anhydride thereof.
  • Suitable ethylenically unsaturated acids and/or anhydrides thereof include, without limitation, acrylic acid, methacrylic acid, itaconic acid, crotonic acid, maleic acid, maleic anhydride, citraconic anhydride, itaconic anhydride, ethylenically unsaturated sulfonic acids and/or anhydrides such as sulfoethyl methacrylate, and half esters of maieic and fumaric acids, such as butyl hydrogen maleate and ethyl hydrogen fumarate in which one carboxyl group is esterified with an alcohol,
  • Examples of other polymerizable ethylenically unsaturated monomers to introduce carboxyl functionality are alkyl including cycloalkyl and aryl (meth)acrylates containing from 1 to 12 carbon atoms in the alkyl group and from 6 to 12 carbon atoms in the aryf group.
  • Specific examples of such monomers include methyl methacrylate, n-butyi methacryiate, n-butyl acrylate, 2-ethylhexyl methacrylate, cyclohexyl methacrylate and phenyl methacrylate.
  • the amount of the polymerizabie carboxyl-containing ethylenically unsaturated monomers is preferably sufficient to provide a carboxy) content of up to 55, preferably 15.0 to 45.0 percent by weight based on the weight of the total monomer combination used to prepare the (meth)acrylic polymer.
  • Preferabiy at least a portion of the carboxyl groups are derived from a carboxylic acid such that the acid value of the polymer is within the range of 20 to 80, preferably 30 to 70, on a 100% resin solids basis.
  • the (meth)acrylic polymer used in the invention also preferably contains hydroxyl functionality typically achieved by using a hydroxyl functional ethyfenically unsaturated poiymerizable monomer.
  • hydroxyl functional ethyfenically unsaturated poiymerizable monomer examples include hydroxyalkyl esters of (meth)acrylic acids having from 2 to 4 carbon atoms in the hydroxyalkyl group. Specific examples include hydroxyethyl (meth)acrylate, hydroxypropyj (meth)acrylate and 4-hydroxybutyl (meth)acrylate.
  • the amount of the hydroxy functional ethylenically unsaturated monomer is sufficient to provide a hydroxy!
  • the (meth)acrylic polymer optionally contains nitrogen functionality introduced from a nitrogen-containing ethylenically unsaturated monomer. Examples of nitrogen functionality are amines, amides, ureas, imidazoles and pyrrolidones.
  • N-containing ethylenically unsaturated monomers are: amino-functional ethylenically unsaturated poiymerizable materials that include, without limitation, p-dimethylamino ethyl styrene, t-butyiaminoethyl (meth)acrylate, dimethyiaminoethyl (meth)acrylate, diethylaminoethyl (meth)acrylate, dimethylaminopropyl (meth)acrylate and dimethylaminopropyl (meth)acrylamide; armido-functional ethylenically unsaturated materials that include acrylamide, methacrylamide, n-methyl acrylamide and n-ethyl (meth)acrylamide; urea functional ethylenically unsaturated monomers that include methacrylamidoethylethyJene urea.
  • the amount of the nitrogen-containing ethylenically unsaturated monomer is sufficient to provide nitrogen content of up to 5 such as from 0.2 to 5.0 , preferably from 0.4 to 2.5 percent by weight based on weight of a total monomer combination used in preparing the (meth)acrylic poJymer.
  • poiymerizable ethyfenically unsaturated monomers that may be used to prepare the (meth)acrylic polymer.
  • examples of such monomers include poly(meth)acryiates such as ethylene glycol di(meth)acrylate, trimethylolpropane tri(meth)acrylate, ditrimethylolpropane tetraacrylate; aromatic vinyl monomers such as styrene, vinyl toluene and alpha- methylstyrene; monoolefinic and diolefinic hydrocarbons, unsaturated esters of organic and inorganic acids and esters of unsaturated acids and nitriles.
  • Examples of such monomers include 1 ,3-butadiene, acrylonitrile, vinyl butyrate, vinyl acetate, allyl chloride, divinyl benzene, diallyl itaconate, triallyl cyanurate as well as mixtures thereof.
  • the polyfunctionaf monomers, such as the polyacrylates, if present, are typically used in amounts up to 20 percent by weight.
  • the monfunctionai monomers, if present, are used in amount up to 70 percent by weight; the percentage being based on weight of the total monomer combination used to prepare the (meth)acrylic polymer.
  • the (meth)acrylic polymer is typically formed by solution polymerization of the ethylenically unsaturated polymerizable monomers in the presence of a polymerization initiator such as azo compounds, such as alpha, alpha'-azobis(isobutyronitrile), 2,2'-azobis (methylbutyronitrile) and 2,2'- azobis(2,4-dimethylvaleronitrile); peroxides, such as benzoyl peroxide, cumene hydroperoxide and t-amylperoxy-2-ethyfhexanoate; tertiary butyl peracetate; tertiary butyl perbenzoate; isopropyl percarbonate; butyl isopropyl peroxy carbonate; and similar compounds.
  • a polymerization initiator such as azo compounds, such as alpha, alpha'-azobis(isobutyronitrile), 2,2'-azobis (methylbutyronitrile) and 2,2'
  • the quantity of initiator employed can be varied considerably; however, in most instances, it is desirable to utilize from 0.1 to 10 percent by weight of initiator based on the total weight of copolymerizabfe monomers employed.
  • a chain modifying agent or chain transfer agent may be added to the polymerization mixture.
  • the mercaptans such as dodecyl mercaptan, tertiary dodecyl mercaptan, octyl mercaptan, hexyi mercaptan and the mercaptoalkyl trialkoxysilanes such as 3- mercaptopropyl trimethoxysilane may be used for this purpose as well as other chain transfer agents such as cyclopentadiene, allyl acetate, allyl carbamate, and mercaptoethanol.
  • chain transfer agents such as cyclopentadiene, allyl acetate, allyl carbamate, and mercaptoethanol.
  • the polymerization reaction for the mixture of monomers to prepare the acrylic polymer can be carried out in an organic solvent medium utilizing conventional solution polymerization procedures which are well known in the addition polymer art as illustrated with particularity in, for example, United States Patent Nos. 2,978,437; 3,079,434 and 3,307,963.
  • Organic solvents that may be utilized in the polymerization of the monomers include virtually any of the organic solvents often employed in preparing acrylic or vinyl polymers such as, for example, alcohols, ketones, aromatic hydrocarbons or mixtures thereof, illustrative of organic solvents of the above type which may be employed are alcohols such as lower alkanols containing 2 to 4 carbon atoms including ethanol, propanoJ, isopropanol, and butanol; ether alcohols such as ethylene glycol monoethyl ether, ethylene glycol monobutyl ether, propylene glycol monomethyl ether, and dipropylene glycol monoethyl ether; ketones such as methyl ethyl ketone, methyl N-butyl ketone, and methyl isobutyl ketone; esters such as butyl acetate; and aromatic hydrocarbons such as xylene, toluene, and naphtha.
  • alcohols such as lower alkanols
  • the polymerization of the ethylenicaily unsaturated components is conducted at from 0 0 C to 150 0 C, such as from 5O 0 C to 150 0 C, or, in some cases, from 8O 0 C to 120°C.
  • the polymer prepared as described above is usually dissolved in solvent and typically has a resin solids content of about 15 to 80, preferably 20 to 60 percent by weight based on total solution weight.
  • the molecular weight of the polymer typically ranges between 3,000 to 1 ,000,000, preferably 5,000 to 100,000 as determined by gel permeation chromatography using a polystyrene standard.
  • the polymer solution such as described above can be mixed with water to initiate the crosslinking reaction and to build viscosity necessary for fiber formation.
  • water typically about 5 to 20, preferably 10 to 15 percent by weight water is added to the polymer solution with the percentage by weight being based on total weight of the polymer solution and the water.
  • a base such as a water-soluble organic amine is added to the water-polymer solution to catalyze the crosslinking reaction.
  • a thickener such as polyvinyl pyrrolidone, polyvinyl alcohol, polyvinyl acetate, polyamides and/or a cellulosic thickener can be added to the electrospinning formulation to better control its viscoelastic behavior. If used, the thickener is present in amounts no greater than 20 percent by weight, typically from 1 to 6 percent by weight based on weight of the polymer solution.
  • the electrospinning formulation prepared as described above is then stored to permit the viscosity to build to the crosslinking reaction.
  • the viscosity is at least 5 and less than 2,000, usually less than 1 ,000, such as preferably within the range of 50 to 250 centistokes for the electrospinning process.
  • a Bubble Viscometer according to ASTM D- 1544 determines the viscosity.
  • the time for storing the electrospinning formulation will depend on a number of factors such as temperature, crosslinking functionality and catalyst. Typically, the electrospinning formulation will be stored for as low as one minute up to two hours.
  • the formulations described above typically produce fibers having a diameter of up to 5,000, such as from 5 to 5,000 nanometers, more typically within the range of 50 to 1 ,200 nanometers, such as 50 to 700 nanometers.
  • the fibers also can have a ribbon configuration and in this case diameter is intended to mean the largest dimension of the fiber.
  • the width of the ribbon shaped fibers is up to 5000 such as 500 to 5000 nanometers and the thickness up to 200 such as 5 to 200 nanometers.
  • the polymer is not completely soluble in tetrahydrofuran.
  • Example B The acrylic-silane resin solution from Example B (8.5 grams) was blended with polyvinylpyrrolidone (0.1 grams) and water (1.5 grams). The formulation was stored at room temperature for 210 minutes. A portion of the resulting solution was loaded into a 10 ml syringe and delivered via a syringe pump at a rate of 0.2 milliliters per hour to the spinneret of Example 1 . The conditions for electrospinning were as described in Example 1 . Ribbon shaped nanofibers having a thickness of 100-200 nanometers and a width of 900-1200 nanometers were collected on grounded aluminum foil and were characterized by optical microscopy and scanning electron microscopy.
  • Example A The acrylic-silane resin from Example A (8.5 grams) was blended with polyvinylpyrrolidone (0,1 grams) and water (1.5 grams). The formulation was stored at room temperature for 225 minutes. A portion of the resulting solution was loaded into a 10 ml syringe and delivered via a syringe pump at a rate of 1.6 milliliters per hour to the spinneret as described in Example 1. The conditions for electrospinning were as described in Example 1 . Ribbon shaped nanofibers having a thickness of 100-200 nanometers and a width of 1200-5000 nanometers were collected on grounded aluminum foil and were characterized by optical microscopy and scanning electron microscopy. A sample of the nanofibers was dried in an oven at 110 0 C for two hours. No measurable weight loss was observed. This indicates the nanofibers were completely crosslinked.

Abstract

A method for electrospinning polymer fibers and the resultant electrospun fibers are disclosed. In the electrospinning method, the polymer undergoes a crosslinking reaction prior to and during the electrospinning process.

Description

ELECTROSPINNING PROCESS
FIELD OF THE INVENTION
[0001] The present invention relates to an electrospinning process, the resulting electrospun fiber and polymers used in the electrospinning process.
BACKGROUND OF THE INVENTION
[0002] The process of electrospinning uses an electrical charge to form fine fibers. The process consists of a spinneret with a dispensing needle, a syringe pump, a power supply and a grounded collection device. Polymers in solution or as melts are located in the syringe and driven to the needle tip by the syringe pump where they form a droplet. When voltage is applied to the needle, a droplet is stretched to an electrified liquid jet. The jet is elongated continuously until it is deposited on the collector as a mat of fine fibers usually of nanometer-sized dimensions. The resultant fibers are useful in a wide variety of applications such as protective clothing, wound dressing and as supports or carriers for catalyst. To form a fiber, the polymeric melt or solution must have a sufficient viscosity otherwise a drop rather than a liquid jet will form. Typically, thickeners are included in the polymer solution or melt to provide the necessary viscosity. However, thickeners can adversely affect the properties of the resultant fibers and for this reason, their use should be minimized.
SUMMARY OF THE INVENTION
[0003] The present invention provides for a process of electrospinning a fiber from an electrically conductive solution of a polymer in the presence of an electric field between a spinneret and a ground source. The polymer undergoes a crosslinking reaction prior to and during the electrospinning process resulting in a viscosity buildup of the polymer solution enabling fiber formation and minimizing the use of thickeners.
[0004] The invention also provides for the resultant eiectrospun fiber that contains silane, preferably carboxyl and hydroxyl groups and optionally a nitrogen-containing group such as amine or amide groups. The silane groups provide for crosslinking and viscosity build-up. The carboxyl, hydroxyl, amine and amide groups provide for a hydrogen bonding and viscosity build-up. The carboxyl group, in the form of carboxylic acid, and the nitrogen-containing groups are good electrical charge carrying groups.
BRIEF DESCRIPTION OF THE DRAWINGS [0005] FIG. 1 depicts a basic electrospinning system,
[0006] FIG. 2 simulates a scanning electron microscopic (SCM) image of a non-woven mat.
DETAILED DESCRIPTION OF THE INVENTION [0007] For purposes of the following detailed description, it is to be understood that the invention may assume various alternative variations and step sequences, except where expressly specified to the contrary. Moreover, other than in any operating examples, or where otherwise indicated, ail numbers expressing, for example, quantities of ingredients used in the specification and claims are to be understood as being modified in all instances by the term "about". Accordingly, unless indicated to the contrary, the numerical parameters set forth in the following specification and attached claims are approximations that may vary depending upon the desired properties to be obtained by the present invention. At the very least, and not as an attempt to limit the application of the doctrine of equivalents to the scope of the claims, each numerical parameter shouid at least be construed in light of the number of reported significant digits and by applying ordinary rounding techniques. Notwithstanding that the numerical ranges and parameters setting forth the broad scope of the invention are approximations, the numerical values set forth in the specific examples are reported as precisely as possible. Any numerical value, however, inherently contains certain errors necessarily resulting from the standard variation found in their respective testing measurements. [0008] Also, it should be understood that any numerical range recited herein is intended to include all sub-ranges subsumed therein. For example, a range of "1 to 10" is intended to include all sub-ranges between (and including) the recited minimum value of 1 and the recited maximum value of 10, that is, having a minimum value equal to or greater than 1 and a maximum value of equal to or less than 10.
[0009] In this application, the use of the singular includes the plural and plural encompasses singular, unless specifically stated otherwise. In addition, in this application, the use of "or" means "and/or" unless specifically stated otherwise, even though "and/or" may be explicitly used in certain instances. [0010] The term "polymer" is also meant to include copolymer and oligiomer. The term "acrylic" is meant to include methacrylic and is depicted by (meth)acrylic.
[0011] With reference to FIG. 1 , the electrospinning system consists of three major components, a power supply 1 , a spinneret 3 and an electrically grounded collector 4. Direct current or alternating current may be used in the electrospinning process. The polymer solution 5 is contained in a syringe 7. A syringe pump 9 forces the solution through the spinneret 3 at a controlled rate. A drop of the solution forms at the tip of the needle 1 1. Upon application of a voltage, typically from 5 to 30 kilovolts (kV), the drop becomes electrically charged. Consequently, the drop experiences electrostatic repulsion between the surface charges and the forces exerted by the external electric field. These electrical forces will distort the drop and will eventually overcome the surface tension of the polymer solution resulting in the ejection of a liquid jet 13 from the tip of the needle 1 1. Because of its charge, the jet is drawn downward to the grounded collector 4. During its travel towards the collector 4, the jet 13 undergoes a stretching action leading to the formation of a thin fiber. The charged fiber is deposited on the collector 4 as a random oriented non-woven mat as generally shown in FIG. 2. [0012] The polymers of the present invention can be acrylic polymers.
As used herein, the term "acrylic" polymer refers to those polymers that are well known to those skilled in the art which results in the polymerization of one or more ethylenically unsaturated polymerizable materials. (Meth)acrylic polymers suitable for use in the present invention can be made by any of a wide variety of methods as will be understood by those skilled in the art. The (meth)acrylic polymers can be made by addition polymerization of unsaturated polymerizable materials that contain silane groups, carboxyl groups, hydroxyl groups and optionally a nitrogen-containing group. Examples of silane groups include, without limitation, groups that have the structure Si-Xn (wherein n is an integer having a value ranging from 1 to 3 and X is selected from chlorine, alkoxy esters, and/or acyloxy esters). Such groups hydroiyze in the presence of water including moisture in the air to form silanol groups that condense to form -Si-O-Si- groups. [0013] Examples of silane-containing ethylenically unsaturated polymerizable materials, suitable for use in preparing such (meth)acrylic polymers include, without limitation, ethylenically unsaturated alkoxy siianes and ethylenically unsaturated acyloxy siianes, more specific examples of which include vinyf siianes such as vinyl trimethoxysilane, acrylatoalkoxysilanes, such as gamma-acryloxypropyl trimethoxysilane and gamma-acryloxypropyl triethoxysilane, and methacrylatoalkoxysilanes, such as gamma-methacryloxypropyl trimethoxysilane, gamma-methacryloxypropyl triethoxysilane and gamma-methacryloxypropy! tris-(2-methoxyethoxy) silane; acyloxysilanes, including, for example, acryfato acetoxysϋanes, methacrylato acetoxysilanes and ethylenically unsaturated acetoxysilanes, such as acrylatopropyl triacetoxysilane and methacrylatopropyi triacetoxysilane. In certain embodiments, it may be desirable to utilize monomers that, upon addition polymerization, will result in a (meth)acrylic polymer in which the Si atoms of the resulting hydrolyzable silyl groups are separated by at least two atoms from the backbone of the polymer. Preferred monomers are (meth)acryloxyaikylpolyalkoxy silane, particularly (meth)acryloxyalkyltrialkoxy silane in which the alkyl group contains from 2 to 3 carbon atoms and the alkoxy groups contain from 1 to 2 carbon atoms. [0014] In certain embodiments, the amount of the silane-containing ethylenically unsaturated polymerizable material used in the total monomer mixture is chosen so as to result in the production of a (meth)acrylic polymer comprising silane groups that contain from 0.2 to 20, preferably 5 to 10 percent by weight, silicon, based on the weight of the total monomer combination used in preparing the (meth)acryiic polymer. [0015] The (meth)acrylic polymer suitable for use in the present invention can be the reaction product of one or more of the aforementioned silane-containing ethylenically unsaturated polymerizable materials and preferably an ethylenically unsaturated poiymerizable material that comprises carboxyl such as carboxylic acid groups or an anhydride thereof. Examples of suitable ethylenically unsaturated acids and/or anhydrides thereof include, without limitation, acrylic acid, methacrylic acid, itaconic acid, crotonic acid, maleic acid, maleic anhydride, citraconic anhydride, itaconic anhydride, ethylenically unsaturated sulfonic acids and/or anhydrides such as sulfoethyl methacrylate, and half esters of maieic and fumaric acids, such as butyl hydrogen maleate and ethyl hydrogen fumarate in which one carboxyl group is esterified with an alcohol,
[0016] Examples of other polymerizable ethylenically unsaturated monomers to introduce carboxyl functionality are alkyl including cycloalkyl and aryl (meth)acrylates containing from 1 to 12 carbon atoms in the alkyl group and from 6 to 12 carbon atoms in the aryf group. Specific examples of such monomers include methyl methacrylate, n-butyi methacryiate, n-butyl acrylate, 2-ethylhexyl methacrylate, cyclohexyl methacrylate and phenyl methacrylate. [0017] The amount of the polymerizabie carboxyl-containing ethylenically unsaturated monomers is preferably sufficient to provide a carboxy) content of up to 55, preferably 15.0 to 45.0 percent by weight based on the weight of the total monomer combination used to prepare the (meth)acrylic polymer. Preferabiy, at least a portion of the carboxyl groups are derived from a carboxylic acid such that the acid value of the polymer is within the range of 20 to 80, preferably 30 to 70, on a 100% resin solids basis. [0018] The (meth)acrylic polymer used in the invention also preferably contains hydroxyl functionality typically achieved by using a hydroxyl functional ethyfenically unsaturated poiymerizable monomer. Examples of such materials include hydroxyalkyl esters of (meth)acrylic acids having from 2 to 4 carbon atoms in the hydroxyalkyl group. Specific examples include hydroxyethyl (meth)acrylate, hydroxypropyj (meth)acrylate and 4-hydroxybutyl (meth)acrylate. The amount of the hydroxy functional ethylenically unsaturated monomer is sufficient to provide a hydroxy! content of up to 6.5 such as 0.5 to 6.5, preferably 1 to 4 percent by weight based on the weight of the total monomer combination used to prepare the (meth)acrylic polymer. [0019] The (meth)acrylic polymer optionally contains nitrogen functionality introduced from a nitrogen-containing ethylenically unsaturated monomer. Examples of nitrogen functionality are amines, amides, ureas, imidazoles and pyrrolidones. Examples of suitable N-containing ethylenically unsaturated monomers are: amino-functional ethylenically unsaturated poiymerizable materials that include, without limitation, p-dimethylamino ethyl styrene, t-butyiaminoethyl (meth)acrylate, dimethyiaminoethyl (meth)acrylate, diethylaminoethyl (meth)acrylate, dimethylaminopropyl (meth)acrylate and dimethylaminopropyl (meth)acrylamide; armido-functional ethylenically unsaturated materials that include acrylamide, methacrylamide, n-methyl acrylamide and n-ethyl (meth)acrylamide; urea functional ethylenically unsaturated monomers that include methacrylamidoethylethyJene urea. [0020] If used, the amount of the nitrogen-containing ethylenically unsaturated monomer is sufficient to provide nitrogen content of up to 5 such as from 0.2 to 5.0 , preferably from 0.4 to 2.5 percent by weight based on weight of a total monomer combination used in preparing the (meth)acrylic poJymer.
[0021] Besides the poiymerizable monomers mentioned above, other poiymerizable ethyfenically unsaturated monomers that may be used to prepare the (meth)acrylic polymer. Examples of such monomers include poly(meth)acryiates such as ethylene glycol di(meth)acrylate, trimethylolpropane tri(meth)acrylate, ditrimethylolpropane tetraacrylate; aromatic vinyl monomers such as styrene, vinyl toluene and alpha- methylstyrene; monoolefinic and diolefinic hydrocarbons, unsaturated esters of organic and inorganic acids and esters of unsaturated acids and nitriles. Examples of such monomers include 1 ,3-butadiene, acrylonitrile, vinyl butyrate, vinyl acetate, allyl chloride, divinyl benzene, diallyl itaconate, triallyl cyanurate as well as mixtures thereof. The polyfunctionaf monomers, such as the polyacrylates, if present, are typically used in amounts up to 20 percent by weight. The monfunctionai monomers, if present, are used in amount up to 70 percent by weight; the percentage being based on weight of the total monomer combination used to prepare the (meth)acrylic polymer. [0022] The (meth)acrylic polymer is typically formed by solution polymerization of the ethylenically unsaturated polymerizable monomers in the presence of a polymerization initiator such as azo compounds, such as alpha, alpha'-azobis(isobutyronitrile), 2,2'-azobis (methylbutyronitrile) and 2,2'- azobis(2,4-dimethylvaleronitrile); peroxides, such as benzoyl peroxide, cumene hydroperoxide and t-amylperoxy-2-ethyfhexanoate; tertiary butyl peracetate; tertiary butyl perbenzoate; isopropyl percarbonate; butyl isopropyl peroxy carbonate; and similar compounds. The quantity of initiator employed can be varied considerably; however, in most instances, it is desirable to utilize from 0.1 to 10 percent by weight of initiator based on the total weight of copolymerizabfe monomers employed. A chain modifying agent or chain transfer agent may be added to the polymerization mixture. The mercaptans, such as dodecyl mercaptan, tertiary dodecyl mercaptan, octyl mercaptan, hexyi mercaptan and the mercaptoalkyl trialkoxysilanes such as 3- mercaptopropyl trimethoxysilane may be used for this purpose as well as other chain transfer agents such as cyclopentadiene, allyl acetate, allyl carbamate, and mercaptoethanol.
[0023] The polymerization reaction for the mixture of monomers to prepare the acrylic polymer can be carried out in an organic solvent medium utilizing conventional solution polymerization procedures which are well known in the addition polymer art as illustrated with particularity in, for example, United States Patent Nos. 2,978,437; 3,079,434 and 3,307,963. Organic solvents that may be utilized in the polymerization of the monomers include virtually any of the organic solvents often employed in preparing acrylic or vinyl polymers such as, for example, alcohols, ketones, aromatic hydrocarbons or mixtures thereof, illustrative of organic solvents of the above type which may be employed are alcohols such as lower alkanols containing 2 to 4 carbon atoms including ethanol, propanoJ, isopropanol, and butanol; ether alcohols such as ethylene glycol monoethyl ether, ethylene glycol monobutyl ether, propylene glycol monomethyl ether, and dipropylene glycol monoethyl ether; ketones such as methyl ethyl ketone, methyl N-butyl ketone, and methyl isobutyl ketone; esters such as butyl acetate; and aromatic hydrocarbons such as xylene, toluene, and naphtha. [0024] In certain embodiments, the polymerization of the ethylenicaily unsaturated components is conducted at from 00C to 1500C, such as from 5O0C to 1500C, or, in some cases, from 8O0C to 120°C. [0025] The polymer prepared as described above is usually dissolved in solvent and typically has a resin solids content of about 15 to 80, preferably 20 to 60 percent by weight based on total solution weight. The molecular weight of the polymer typically ranges between 3,000 to 1 ,000,000, preferably 5,000 to 100,000 as determined by gel permeation chromatography using a polystyrene standard.
[0026] For the electrospinning application, the polymer solution such as described above can be mixed with water to initiate the crosslinking reaction and to build viscosity necessary for fiber formation. Typically about 5 to 20, preferably 10 to 15 percent by weight water is added to the polymer solution with the percentage by weight being based on total weight of the polymer solution and the water. Preferably a base such as a water-soluble organic amine is added to the water-polymer solution to catalyze the crosslinking reaction. Optionally a thickener such as polyvinyl pyrrolidone, polyvinyl alcohol, polyvinyl acetate, polyamides and/or a cellulosic thickener can be added to the electrospinning formulation to better control its viscoelastic behavior. If used, the thickener is present in amounts no greater than 20 percent by weight, typically from 1 to 6 percent by weight based on weight of the polymer solution.
[0027] The electrospinning formulation prepared as described above is then stored to permit the viscosity to build to the crosslinking reaction. When the viscosity is sufficiently high but short of gelation, the formulation is subjected to the electrospinning process as described above. [0028] Typically, the viscosity is at least 5 and less than 2,000, usually less than 1 ,000, such as preferably within the range of 50 to 250 centistokes for the electrospinning process. A Bubble Viscometer according to ASTM D- 1544 determines the viscosity. The time for storing the electrospinning formulation will depend on a number of factors such as temperature, crosslinking functionality and catalyst. Typically, the electrospinning formulation will be stored for as low as one minute up to two hours. [0029] When subject to the electrospinning process, the formulations described above typically produce fibers having a diameter of up to 5,000, such as from 5 to 5,000 nanometers, more typically within the range of 50 to 1 ,200 nanometers, such as 50 to 700 nanometers. The fibers also can have a ribbon configuration and in this case diameter is intended to mean the largest dimension of the fiber. Typically the width of the ribbon shaped fibers is up to 5000 such as 500 to 5000 nanometers and the thickness up to 200 such as 5 to 200 nanometers.
[0030] The following examples are presented to demonstrate the genera! principles of the invention. However, the invention should not be considered as limited to the specific examples presented. All parts are by weight unless otherwise indicated. EXAMPLES A, B and C
Synthesis of Acrylic Silaπe Polymers
[0031] For each of Examples A to C in Tabfe 1 below, a reaction flask was equipped with a stirrer, thermocouple, nitrogen inlet and a condenser. Charge A was then added and stirred with heat to reflux temperature (75°C- 80°C) under nitrogen atmosphere. To the refluxing ethanol, charge B and charge C were simultaneously added over three hours. The reaction mixture was held at reflux condition for two hours. Charge D was then added over a period of 30 minutes. The reaction mixture was held at reflux condition for two hours and subsequently cooled to 300C.
TABLE 1
Figure imgf000012_0001
, , d Co.
2 gamma-methacryloxypropyltrimethoxysilane, available from GE silicones.
3 Di-trimethylolpropane tetraacrylate, available from Sartomer Company Inc.
4 2,2'-azo bis(2-methyl butyronitrile), available from E.I. duPont de Nemours & Co., Inc.
5 Mn of soluble portion; the polymer is not completely soluble in tetrahydrofuran.
EXAMPLES 1 , 2 AND 3
AcrylioSilane Nanofibers
Example 1
[0032] The acrylic-silane resin solution from Example C (8.5 grams) was blended with polyvinylpyrrolidone (0.2 grams) and water (1.5 grams). The formulation was stored at room temperature for 215 minutes. A portion of the resulting formulation was loaded into a 10 ml syringe and delivered via a syringe pump at a rate of 1.6 milliliters per hour to a spinneret (stainless steel tube 1/16-inch outer diameter and 0.010-inch internal diameter). This tube was connected to a grounding aluminum collector via a high voltage source to which about 21 kV potential was applied. The delivery tube and collector were encased in a box that allowed nitrogen purging to maintain a relative humidity of less than 25%. Ribbon shaped nanofibers having a thickness of about 100-200 nanometers and a width of 500-700 nanometers were collected on the grounded aluminum panels and were characterized by optical microscopy and scanning electron microscopy.
Example 2
[0033] The acrylic-silane resin solution from Example B (8.5 grams) was blended with polyvinylpyrrolidone (0.1 grams) and water (1.5 grams). The formulation was stored at room temperature for 210 minutes. A portion of the resulting solution was loaded into a 10 ml syringe and delivered via a syringe pump at a rate of 0.2 milliliters per hour to the spinneret of Example 1 . The conditions for electrospinning were as described in Example 1 . Ribbon shaped nanofibers having a thickness of 100-200 nanometers and a width of 900-1200 nanometers were collected on grounded aluminum foil and were characterized by optical microscopy and scanning electron microscopy.
Example 3
[0034] The acrylic-silane resin from Example A (8.5 grams) was blended with polyvinylpyrrolidone (0,1 grams) and water (1.5 grams). The formulation was stored at room temperature for 225 minutes. A portion of the resulting solution was loaded into a 10 ml syringe and delivered via a syringe pump at a rate of 1.6 milliliters per hour to the spinneret as described in Example 1. The conditions for electrospinning were as described in Example 1 . Ribbon shaped nanofibers having a thickness of 100-200 nanometers and a width of 1200-5000 nanometers were collected on grounded aluminum foil and were characterized by optical microscopy and scanning electron microscopy. A sample of the nanofibers was dried in an oven at 1100C for two hours. No measurable weight loss was observed. This indicates the nanofibers were completely crosslinked.
[0035] Whereas particular embodiments of this invention have been described above for purposes of illustration, it will be evident to those skilled in the art that numerous variations of the details of the present invention may be made without departing from the invention as defined in the appended claims.

Claims

WHAT IS CLAIMED IS:
1. A method for eiectrospinning a fiber from an electrically conducting solution of polymer in the presence of an electric field between a spinneret and a ground source, the polymer undergoing a crosslinking reaction prior to and during eiectrospinning.
2. The method of claim 1 in which the polymer contains crosslinkable groups along the polymer backbone.
3. The method of claim 2 in which the crosslinkable groups are reactive with moisture.
4. The method of claim 3 in which the crossiinkable groups are siiane groups.
5. The method of claim 2 in which the polymer is a (meth)acrylic polymer,
6. The method of claim 2 in which the polymer is a (meth)acrylic polymer containing siiane groups.
7. The method of claim 2 in which the polymer, besides containing crosslinkable groups, also contains groups selected from carboxyl and hydroxy!.
8. The method of claim 2 in which the polymer contains sϋane groups, carboxyl groups, hydroxy) groups and nitrogen-containing groups.
9. The method of claim 2 in which the siiane groups are present in the polymer in amounts of 0.2 to 20 percent by weight silicon based on total polymer weight.
10. The method of claim 8 in which the polymer contains from:
(a) 0.2 to 20 percent silane group measured as silicon,
(b) 1 to 45 percent carboxyl groups,
(c) 0.5 to 6.5 percent hydroxyl groups, and
(d) 0.2 to 5,0 percent nitrogen groups; the percentages by weight being based on total polymer weight.
1 1 . The method of claim 1 in which the solution contains a thickener.
12. The method of claim 1 1 in which the thickener is polyvinyl pyrrolidone.
13. The method of claim 12 in which the polyvinyl pyrrolidone is present in amounts of no greater than 20 percent by weight based on total weight of solution.
14. An electrospun fiber comprising a polymer that has been crosslinked prior to and during the electrospinning process.
15. The electrospun fiber of claim 14 having a diameter of from 5 to 5,000 nanometers.
16. The electrospun fiber of claim 14 having -Si-O-Si- crosslinks.
17. The electrospun fiber of claim 14 being a crosslinked (meth)acrylic polymer.
18. The electrospun fiber of claim 14 being a (meth)acrylic polymer with -Si-O-Si- crosslinks.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010025381A2 (en) * 2008-08-29 2010-03-04 Dow Corning Corporation Article formed from electrospinning a dispersion
WO2010108124A2 (en) * 2009-03-19 2010-09-23 Nanostatics Corporation Fluid formulations for electric-field-driven spinning of fibers
US8715828B2 (en) 2008-08-29 2014-05-06 Dow Corning Corporation Emulsion of metallized particles comprising a compound having a pendant Si-H group
US9428847B2 (en) 2010-05-29 2016-08-30 Nanostatics Corporation Apparatus, methods, and fluid compositions for electrostatically-driven solvent ejection or particle formation

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2911151B1 (en) * 2007-01-05 2010-08-20 Rhodia Poliamida E Especialidades Ltda PROCESS FOR OBTAINING A PRODUCT CONTAINING NANOFIBERS AND PRODUCT COMPRISING NANOFIBRES
RU2497983C2 (en) * 2008-06-24 2013-11-10 Стелленбош Юниверсити Method and apparatus for producing fine fibres
WO2011127218A2 (en) 2010-04-06 2011-10-13 Ndsu Research Foundation Liquid silane-based compositions and methods for producing silicon-based materials
JP2015514876A (en) * 2011-10-03 2015-05-21 エヌディーエスユー リサーチ ファウンデーション Liquid silane composition and processing method
WO2014137095A1 (en) * 2013-03-08 2014-09-12 (주)에프티이앤이 Filter medium having nanofibers on both sides of base and having improved heat resistance, and manufacturing method therefor
US10870928B2 (en) 2017-01-17 2020-12-22 Ian McClure Multi-phase, variable frequency electrospinner system
EP3570821B1 (en) 2017-01-23 2021-07-21 AFYX Therapeutics A/S Method for fabrication of a two-layered product based on electrospun fibres
CN114541038B (en) * 2020-11-24 2023-12-12 诺一迈尔(苏州)医学科技有限公司 Preparation method of electrostatic spinning membrane for repairing tissue defect

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005026398A2 (en) 2003-09-05 2005-03-24 Board Of Supervisors Of Louisiana State University And Agricultural And Mechanical College Nanofibers, and apparatus and methods for fabricating nanofibers by reactive electrospinning

Family Cites Families (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03220305A (en) * 1989-11-21 1991-09-27 I C I Japan Kk Production of antistatic spun yarn
JPH09324319A (en) * 1996-06-04 1997-12-16 Nippon Shokubai Co Ltd Transparent fiber and its production
US6265333B1 (en) * 1998-06-02 2001-07-24 Board Of Regents, University Of Nebraska-Lincoln Delamination resistant composites prepared by small diameter fiber reinforcement at ply interfaces
JP3056485B1 (en) * 1999-05-27 2000-06-26 オーケー化成株式会社 Pattern material for synthetic resin
US6743273B2 (en) * 2000-09-05 2004-06-01 Donaldson Company, Inc. Polymer, polymer microfiber, polymer nanofiber and applications including filter structures
US6713011B2 (en) * 2001-05-16 2004-03-30 The Research Foundation At State University Of New York Apparatus and methods for electrospinning polymeric fibers and membranes
US7105124B2 (en) * 2001-06-19 2006-09-12 Aaf-Mcquay, Inc. Method, apparatus and product for manufacturing nanofiber media
US7390452B2 (en) * 2002-03-08 2008-06-24 Board Of Regents, The University Of Texas System Electrospinning of polymer and mesoporous composite fibers
DE50211962D1 (en) * 2002-05-28 2008-05-08 Hollingsworth & Vose Gmbh filter media
US20060024483A1 (en) * 2004-07-29 2006-02-02 Koch William J Transparent composite panel
US20070251421A1 (en) * 2004-09-01 2007-11-01 Rukavina Thomas G Powder coatings prepared from polyurethanes and poly(ureaurethane)s, coated articles and methods of making the same
US8399094B2 (en) * 2004-09-01 2013-03-19 Ppg Industries Ohio, Inc. Multilayer laminated articles including polyurethane and/or poly(ureaurethane) layers and methods of making the same
US20070148471A1 (en) * 2004-09-01 2007-06-28 Rukavina Thomas G Impact resistant polyurethane and poly(ureaurethane) articles and methods of making the same
US20090280329A1 (en) * 2004-09-01 2009-11-12 Ppg Industries Ohio, Inc. Polyurethanes, Articles and Coatings Prepared Therefrom and Methods of Making the Same
US8889815B2 (en) * 2004-09-01 2014-11-18 Ppg Industries Ohio, Inc. Reinforced polyurethanes and poly(ureaurethane)s, methods of making the same and articles prepared therefrom
US20070225468A1 (en) * 2004-09-01 2007-09-27 Rukavina Thomas G Polyurethanes prepared from polyester polyols and/or polycaprolactone polyols, articles and coatings prepared therefrom and methods of making the same
US20070167601A1 (en) * 2004-09-01 2007-07-19 Rukavina Thomas G Polyurethanes prepared from polycarbonate polyols, articles and coatings prepared therefrom and methods of making the same
US8604153B2 (en) * 2004-09-01 2013-12-10 Ppg Industries Ohio, Inc. Poly(ureaurethane)s, articles and coatings prepared therefrom and methods of making the same
US20070173601A1 (en) * 2004-09-01 2007-07-26 Rukavina Thomas G Polyurethanes, articles and coatings prepared therefrom and methods of making the same
US20070167600A1 (en) * 2004-09-01 2007-07-19 Rukavina Thomas G Polyurethanes prepared from polycaprolactone polyols, articles and coatings prepared therefrom and methods of making the same
US8927675B2 (en) * 2004-09-01 2015-01-06 Ppg Industries Ohio, Inc. Poly(ureaurethane)s, articles and coatings prepared therefrom and methods of making the same
US8734951B2 (en) * 2004-09-01 2014-05-27 Ppg Industries Ohio, Inc. Polyurethanes, articles and coatings prepared therefrom and methods of making the same
US9598527B2 (en) * 2004-09-01 2017-03-21 Ppg Industries Ohio, Inc. Polyurethanes, articles and coatings prepared therefrom and methods of making the same
US8653220B2 (en) * 2004-09-01 2014-02-18 Ppg Industries Ohio, Inc. Poly(ureaurethane)s, articles and coatings prepared therefrom and methods of making the same
US20070149749A1 (en) * 2004-09-01 2007-06-28 Rukavina Thomas G Polyurethanes prepared from polycarbonate polyols, articles and coatings prepared therefrom and methods of making the same
US8399559B2 (en) * 2004-09-01 2013-03-19 Ppg Industries Ohio, Inc. Polyurethanes, articles and coatings prepared therefrom and methods of making the same
US20090280709A1 (en) * 2004-09-01 2009-11-12 Ppg Industries Ohio, Inc. Polyurethanes, Articles and Coatings Prepared Therefrom and Methods of Making the Same
US8349986B2 (en) * 2004-09-01 2013-01-08 Ppg Industries Ohio, Inc. Poly(ureaurethane)s, articles and coatings prepared therefrom and methods of making the same
US8207286B2 (en) * 2004-09-01 2012-06-26 Ppg Industries Ohio, Inc Methods for preparing polyurethanes
US8859680B2 (en) * 2004-09-01 2014-10-14 Ppg Industries Ohio, Inc Poly(ureaurethane)s, articles and coatings prepared therefrom and methods of making the same
US8933166B2 (en) * 2004-09-01 2015-01-13 Ppg Industries Ohio, Inc. Poly(ureaurethane)s, articles and coatings prepared therefrom and methods of making the same
AU2006214371A1 (en) * 2005-02-15 2006-08-24 Virginia Commonwealth University Mineral technologies (MT) for acute hemostasis and for the treatment of acute wounds and chronic ulcers
DE102005008926A1 (en) * 2005-02-24 2006-11-16 Philipps-Universität Marburg Process for the preparation of nano- and mesofibres by electrospinning of colloidal dispersions
JP2006283240A (en) * 2005-04-01 2006-10-19 Oji Paper Co Ltd Web-producing apparatus
US8455088B2 (en) * 2005-12-23 2013-06-04 Boston Scientific Scimed, Inc. Spun nanofiber, medical devices, and methods
EP2455453A1 (en) * 2006-09-06 2012-05-23 Corning Incorporated Substrate for immobilizing cells or tissue
US7632563B2 (en) * 2006-12-14 2009-12-15 Ppg Industries Ohio, Inc. Transparent composite articles

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005026398A2 (en) 2003-09-05 2005-03-24 Board Of Supervisors Of Louisiana State University And Agricultural And Mechanical College Nanofibers, and apparatus and methods for fabricating nanofibers by reactive electrospinning

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010025381A2 (en) * 2008-08-29 2010-03-04 Dow Corning Corporation Article formed from electrospinning a dispersion
WO2010025381A3 (en) * 2008-08-29 2010-07-22 Dow Corning Corporation Article formed from electrospinning a dispersion
US8715828B2 (en) 2008-08-29 2014-05-06 Dow Corning Corporation Emulsion of metallized particles comprising a compound having a pendant Si-H group
WO2010108124A2 (en) * 2009-03-19 2010-09-23 Nanostatics Corporation Fluid formulations for electric-field-driven spinning of fibers
WO2010108124A3 (en) * 2009-03-19 2011-01-13 Nanostatics Corporation Fluid formulations for electric-field-driven spinning of fibers
US8518319B2 (en) 2009-03-19 2013-08-27 Nanostatics Corporation Process of making fibers by electric-field-driven spinning using low-conductivity fluid formulations
US9428847B2 (en) 2010-05-29 2016-08-30 Nanostatics Corporation Apparatus, methods, and fluid compositions for electrostatically-driven solvent ejection or particle formation

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CA2671499A1 (en) 2008-06-19
AU2007333369A1 (en) 2008-06-19
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AU2007333369B2 (en) 2010-11-25
EP2102394B1 (en) 2010-09-15
RU2435876C2 (en) 2011-12-10
RU2009126755A (en) 2011-01-20
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US20080145655A1 (en) 2008-06-19
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